Mixture of Hexanoic acid, ethyl ester + Methyl Alcohol

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Hexanoic acid, ethyl ester

Name
Hexanoic acid, ethyl ester
InChI
InChI=1S/C8H16O2/c1-3-5-6-7-8(9)10-4-2/h3-7H2,1-2H3
InChI Key
SHZIWNPUGXLXDT-UHFFFAOYSA-N
Formula
C8H16O2
SMILES
CCCCCC(=O)OCC
Mol. Weight (g/mol)
144.21
CAS
123-66-0

Methyl Alcohol

Name
Methyl Alcohol
InChI
InChI=1S/CH4O/c1-2/h2H,1H3
InChI Key
OKKJLVBELUTLKV-UHFFFAOYSA-N
Formula
CH4O
SMILES
CO
Mol. Weight (g/mol)
32.04
CAS
67-56-1
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Datasets

  1. η - Viscosity, Pa*s (2)
  2. ρl - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Hexanoic acid, ethyl ester (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0006
293.15 0.0902 0.0006
293.15 0.2147 0.0006
293.15 0.3046 0.0006
293.15 0.4008 0.0007
293.15 0.5031 0.0007
293.15 0.6098 0.0007
293.15 0.7106 0.0007
293.15 0.8074 0.0008
293.15 0.9105 0.0008
293.15 1.0000 0.0008
303.15 0.0000 0.0005
303.15 0.0902 0.0005
303.15 0.2147 0.0005
303.15 0.3046 0.0006
303.15 0.4008 0.0006
303.15 0.5031 0.0006
303.15 0.6098 0.0006
303.15 0.7106 0.0006
303.15 0.8074 0.0007
303.15 0.9105 0.0007
303.15 1.0000 0.0007
313.15 0.0000 0.0004
313.15 0.0902 0.0005
313.15 0.2147 0.0005
313.15 0.3046 0.0005
313.15 0.4008 0.0005
313.15 0.5031 0.0005
313.15 0.6098 0.0005
313.15 0.7106 0.0006
313.15 0.8074 0.0006
313.15 0.9105 0.0006
313.15 1.0000 0.0006

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Hexanoic acid, ethyl ester (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0006
293.15 0.0902 0.0006
293.15 0.2147 0.0006
293.15 0.3046 0.0006
293.15 0.4008 0.0007
293.15 0.5031 0.0007
293.15 0.6098 0.0007
293.15 0.7106 0.0007
293.15 0.8074 0.0008
293.15 0.9105 0.0008
293.15 1.0000 0.0008
303.15 0.0000 0.0005
303.15 0.0902 0.0005
303.15 0.2147 0.0005
303.15 0.3046 0.0006
303.15 0.4008 0.0006
303.15 0.5031 0.0006
303.15 0.6098 0.0006
303.15 0.7106 0.0006
303.15 0.8074 0.0007
303.15 0.9105 0.0007
303.15 1.0000 0.0007
313.15 0.0000 0.0004
313.15 0.0902 0.0005
313.15 0.2147 0.0005
313.15 0.3046 0.0005
313.15 0.4008 0.0005
313.15 0.5031 0.0005
313.15 0.6098 0.0005
313.15 0.7106 0.0006
313.15 0.8074 0.0006
313.15 0.9105 0.0006
313.15 1.0000 0.0006

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Hexanoic acid, ethyl ester (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 791.08
293.15 0.0902 799.01
293.15 0.2147 809.96
293.15 0.3046 817.86
293.15 0.4008 826.32
293.15 0.5031 835.32
293.15 0.6098 844.7
293.15 0.7106 853.56
293.15 0.8074 862.07
293.15 0.9105 871.14
293.15 1.0000 879.01
303.15 0.0000 781.95
303.15 0.0902 789.83
303.15 0.2147 800.71
303.15 0.3046 808.56
303.15 0.4008 816.96
303.15 0.5031 825.9
303.15 0.6098 835.22
303.15 0.7106 844.03
303.15 0.8074 852.48
303.15 0.9105 861.49
303.15 1.0000 869.31
313.15 0.0000 772.01
313.15 0.0902 780.24
313.15 0.2147 791.61
313.15 0.3046 799.81
313.15 0.4008 808.59
313.15 0.5031 817.93
313.15 0.6098 827.67
313.15 0.7106 836.87
313.15 0.8074 845.7
313.15 0.9105 855.11
313.15 1.0000 863.28

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Hexanoic acid, ethyl ester (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 791.08
293.15 0.0902 799.01
293.15 0.2147 809.96
293.15 0.3046 817.86
293.15 0.4008 826.32
293.15 0.5031 835.32
293.15 0.6098 844.7
293.15 0.7106 853.56
293.15 0.8074 862.07
293.15 0.9105 871.14
293.15 1.0000 879.01
303.15 0.0000 781.95
303.15 0.0902 789.83
303.15 0.2147 800.71
303.15 0.3046 808.56
303.15 0.4008 816.96
303.15 0.5031 825.9
303.15 0.6098 835.22
303.15 0.7106 844.03
303.15 0.8074 852.48
303.15 0.9105 861.49
303.15 1.0000 869.31
313.15 0.0000 772.01
313.15 0.0902 780.24
313.15 0.2147 791.61
313.15 0.3046 799.81
313.15 0.4008 808.59
313.15 0.5031 817.93
313.15 0.6098 827.67
313.15 0.7106 836.87
313.15 0.8074 845.7
313.15 0.9105 855.11
313.15 1.0000 863.28

Sources